CN110121479A - For controlling the distribution utensil of the formation of foam during the distribution by fermented beverage (MFBF) concentrate of the mixing based on malt and the MBFB of carbonic acid diluent produced in situ - Google Patents
For controlling the distribution utensil of the formation of foam during the distribution by fermented beverage (MFBF) concentrate of the mixing based on malt and the MBFB of carbonic acid diluent produced in situ Download PDFInfo
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- CN110121479A CN110121479A CN201780080744.0A CN201780080744A CN110121479A CN 110121479 A CN110121479 A CN 110121479A CN 201780080744 A CN201780080744 A CN 201780080744A CN 110121479 A CN110121479 A CN 110121479A
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- mbfb
- concentrate
- core
- diluent
- distribution
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/0042—Details of specific parts of the dispensers
- B67D1/0043—Mixing devices for liquids
- B67D1/0051—Mixing devices for liquids for mixing outside the nozzle
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/44—Mixers in which the components are pressed through slits
- B01F25/442—Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation
- B01F25/4422—Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation the surfaces being maintained in a fixed but adjustable position, spaced from each other, therefore allowing the slit spacing to be varied
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/0015—Apparatus or devices for dispensing beverages on draught the beverage being prepared by mixing at least two liquid components
- B67D1/0021—Apparatus or devices for dispensing beverages on draught the beverage being prepared by mixing at least two liquid components the components being mixed at the time of dispensing, i.e. post-mix dispensers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/0042—Details of specific parts of the dispensers
- B67D1/0043—Mixing devices for liquids
- B67D1/0044—Mixing devices for liquids for mixing inside the dispensing nozzle
- B67D1/0046—Mixing chambers
- B67D1/0047—Mixing chambers with movable parts, e.g. for stirring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/0042—Details of specific parts of the dispensers
- B67D1/0078—Ingredient cartridges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/0042—Details of specific parts of the dispensers
- B67D1/0078—Ingredient cartridges
- B67D1/008—Gas cartridges or bottles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/04—Apparatus utilising compressed air or other gas acting directly or indirectly on beverages in storage containers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/08—Details
- B67D1/12—Flow or pressure control devices or systems, e.g. valves, gas pressure control, level control in storage containers
- B67D1/127—Froth control
- B67D1/1272—Froth control preventing froth
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
- B67D1/00—Apparatus or devices for dispensing beverages on draught
- B67D1/08—Details
- B67D1/12—Flow or pressure control devices or systems, e.g. valves, gas pressure control, level control in storage containers
- B67D1/14—Reducing valves or control taps
- B67D1/1405—Control taps
- B67D1/1411—Means for controlling the build-up of foam in the container to be filled
- B67D1/1416—Means for controlling the build-up of foam in the container to be filled comprising foam inducing means
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- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Devices For Dispensing Beverages (AREA)
Abstract
The present invention relates to distribution utensils, it is used for by preparing and distributing MBFB for being mixed based on the fermented beverage of malt (MBFB) concentrate with carbonic acid diluent, the distribution utensil includes the mixing chamber (2) for mixing MBFB concentrate and carbonic acid diluent, the mixing chamber is defined by wall and is divided into upper and lower part by the mid-plane M1 perpendicular to longitudinal axis X, the mixing chamber includes: (a) concentrate opening (1d), is located in the top and is provided with the fixation device for the fixed container for accommodating MBFB concentrate；(b) diluent openings (4d), it is located in top and is provided with the diluent interconnecting piece connecting with carbonic acid diluent source, (c) (2d) is exported, it is parallel to longitudinal axis X and orients and be located in lower part, for discharging the MBFB of the mixture including MBFB concentrate and carbonic acid diluent, (d) core (2c), it is defined by wicking surface and is mounted in room, so that wicking surface defines flow channel (2p) together with the wall of room, the flow channel has the width w measured perpendicular to wicking surface, it is characterized in that, core is movably mounted in room, core is translated along longitudinal axis X, so as to control flow channel part width w.
Description
Technical field
The present invention relates to beverage dispensing appliance (beverage dispensing appliance), it is used for by by carbon
Sour liquid diluent (carbonated liquid diluent) mixes to be formed in situ and distribute and be based on wheat with MBFC concentrate
The fermented beverage (malt based fermented beverage) (MBFB) of bud.Through the MBFC that is thusly-formed in distribution
The level of the foam (froth) of formation can be controlled easily.
Background of invention
In recent years, the home dispensing appliance used for family has become very popular.Between 1.5 liters and 12 liters
The smaller container of range is produced by many winerys now, and is readily available in shop.With keg phase used in bar
Than the reduction of the small bucket volume used for family causes the packing cost of per unit volume beer to dramatically increase.
In addition, presently, there are the trend of fan's type of beverage (fancier kinds of beverages), wherein
Various beverages component or beverage add each other, and consumer is allowed to generate the composition for oneself for being suitble to its taste at home.
The trend applies also for fermented beverage, such as the fermented beverage (MBFB) based on malt, the beer of such as various tastes and type.
On the one hand it reduces the packing cost of per unit volume beer and on the other hand provides a large amount of (a for consumer
Large palette of) a kind of mode of composition is to provide the container filled with MBFB concentrate, and which can
Be used alone or each other blending and liquid dilution dilution agent.Container can be in the form of unit dose, such as capsule or soft
It wraps (pad).By mixing such MBFB concentrate with liquid diluent, it can generate in situ and supply desired drink simultaneously
Material.Liquid diluent adds and is mixed into unit dose and usually carries out in distribution utensil.
The example of such distribution utensil is coffee dispenser, wherein before being supplied, hot water under stress by
Force the ground coffee bed for penetrating through and being contained in such unit dose.Similar distributing equipment, which is present in, makes tea.In this way
Another example of distributing equipment be Soda water machine (soda machine), be commonly used for fast food restaurant and elsewhere,
These places, consumer can fill its glass with the soda water that he selects from soda water option, all these all
To be obtained from the same distributor.In such dispenser for carbonated water, as the target soda water being contained in various pouches
The fruit juice of conc forms mix in the target soda water that distribution is thusly-formed with carbonated drink (sparkling water).In this way
Dispenser for carbonated water be advantageous because the size of fruit juice pouch is than corresponding ready-to-drink soda water (ready to drink
Soda) much smaller, and therefore transport and store considerably cheaper.
Many winerys have been attempted with fermented beverage to realize allocation plan identical with soda water, but so far
It is non-to be typically restricted to not succeed.These reasons to fail repeatedly, which may be fermented beverage, is more difficult concentration and long than soda fruit juice
Time saves.In fact, have been observed that the fast degradation of contained protein in beer concentrate, this in soda fruit juice not
Occur.Have been proposed solving the solution of the degradation problem, such as in EP number of patent application 16163061.
The produced in situ of MBFB and the example then distributed include the MBFB that will be stored in one or several containers dense
Contracting object is mixed with carbonic acid diluent, the carbonic acid diluent be usually carbonated water or with suitable neutral mouthfeel feature based on carbon
The beer of acid.Carbonic acid diluent is to include higher than the CO of the concentration of the saturation degree in room temperature and atmospheric pressure2Liquid.It is usually
It stores or produces in situ in the pressure for being higher than atmospheric pressure, so that CO2It is dissolved in liquid diluent.It is in mixing chamber that carbonic acid is dilute
When releasing agent and mixing with MBFB concentrate, pressure drop may cause CO2Foam and foam are formed in mixing chamber before dispensing
(foam).The foam of formation and the amount of foam of course depend upon CO2Concentration, temperature and pressure, but it is also relied on and carbon
The composition of the MBFB concentrate of sour diluent mixing.Therefore, for the distribution utensil designed for distributing various MBFB, it is impossible to
The equipment in factory is adjusted to form the foam for the desired amount for being suitable for all MBFB types." impose uniformity without examining individual cases (one size
Fits them all) " system be not suitable for herein.
It will desirably provide by mixing carbonic acid diluent with various MBFB concentrates and distribute the distributor of MBFB
Tool, the distribution utensil can adjust the amount of the foam generated during the charging of MBFB is assigned in vessel.The present invention proposes
Meet the solution of such target.When with reference to the accompanying drawings, be described in detail and appended claims from the point of view of when, these mesh of the invention
And other purposes will be apparent.
Summary of the invention
The present invention limits in the appended independent claim.Preferred embodiment is limited in the dependent claims.It is special
Not, it the present invention relates to distribution utensil, is used for by diluting fermented beverage (MBFB) concentrate based on malt and carbonic acid
Agent mixes to prepare and distribute MBFB, and the distribution utensil includes the mixing for mixing MBFB concentrate and carbonic acid diluent
Room, the mixing chamber are defined by wall and are divided into upper and lower part, the mixing chamber packet by the mid-plane M1 perpendicular to longitudinal axis X
It includes:
(a) concentrate is open, and is located in top and is provided with consolidating for the fixed container for accommodating MBFB concentrate
Determine device；
(b) diluent openings are located in top and are provided with the diluent interconnecting piece connecting with carbonic acid diluent source,
(c) it exports, is parallel to longitudinal axis X and orients and be located in lower part, include MBFB concentrate and carbonic acid for discharging
The MBFB of the mixture of diluent,
(d) core is defined by wicking surface and is mounted in room, and it is logical that such wicking surface defines flowing together with the wall of room
Road, the flow channel have the width w measured perpendicular to wicking surface,
It is characterized in that, core is movably mounted in room, core is translated, along longitudinal axis X to control flowing
The width w of the part in channel.
In order to drive MBFB concentrate outflow container to enter in mixing chamber, it is preferred that distribution utensil further includes that can connect
To the flue of pressurized-gas source, which is arranged so that the outlet of the flue and is fixed to fixed device, appearance
Receive MBFB concentrate container Inner Constitution be in fluid communication.
In order to avoid the unexpected pressure drop in flow channel, it is preferred that the geometry of core makes wicking surface at least
70% is substantially parallel to the wall of room.In preferred embodiments, core reduces flowing along the translation on longitudinal axis X towards top and leads to
The width w of part of the road at concentrate opening and the level height of both diluent openings.By translating core along longitudinal axis X,
The width w of flow channel can preferably between 0.1mm≤w≤10mm, preferably between 0.5mm≤w≤5mm, it is more excellent
Selection of land locally changes between 1mm≤w≤3mm.In some embodiments, wicking surface can contact the wall of mixing chamber, and
And it is one or more in the outlet of such as sealing concentrate opening and/or diluent openings and/or mixing chamber.
In order to preferably control the mixing ratio of concentrate Yu carbonic acid diluent, it is preferred that concentrate opening and diluent
Both openings are both provided with volumetric flow controller, such as positive displacement pump or valve.If the wall of wicking surface and/or mixing chamber is by structure
Chemical conversion has protruding portion and/or recess, then the mixing of MBFB concentrate and carbonic acid diluent can be enhanced.Such structuring
Surface also reduces the formation of turbulent flow.
Core can be translated along the longitudinal axis by one of following preferred embodiment:
Manually or by motor driving rack-and-pinion,
Control stick；Or
Linear motor.
Selectively, according to the composition of the concentrate accommodated in the container, the position of core can be fixed to fixed dress
It is set when setting by container.For example, core connection dress has can be set in the part for being directly facing concentrate opening of wicking surface
Set (core coupling means), the core coupling arrangement be suitable for being reversibly coupled to be mounted on condensate container and
Extend the complementary connecting device of predetermined distance from the opening of the condensate container.When condensate container is fixed to admittedly
When determining device, and when complementary connecting device is reversibly coupled to core coupling arrangement at the part of wicking surface, this is pre-
Fixed distance defines core along the position of longitudinal axis X.
The present invention relates to distribution utensils itself, but further relate to the distribution utensil of ready for use, which, which has, fixes
To fixed device, receiving MBFB concentrate container, and it is connected to carbonic acid diluent (the preferably carbon of diluent interconnecting piece
Sour water) source.If MBFB is pressurized, gas-pressurized (preferably CO2) source may be coupled to flue.
The invention further relates to for controlling the foam formed during the distribution of the fermented beverage (MBFB) based on malt
The method of amount, the described method comprises the following steps:
(a) distribution utensil as defined above is provided；
(b) core is set as the initial position relative to mid-plane M1,
It (c) will be in MBFB concentrate and carbonic acid diluent injection mixing chamber with predetermined volume ratio；And by what is be thusly-formed
MBFB is assigned in container from outlet；
(d) level of the foam formed in accommodating MBFB in a reservoir is assessed,
If (e) level of foam is not corresponding with desired level, X translates core in a longitudinal direction, and
(f) level of step (a) to step (d), until reaching desired foam is repeated.
Brief description
It is described below with reference to being taken in conjunction with attached drawing in order to which essence of the invention is more fully understood, in the accompanying drawings:
Fig. 1: the front view and side view of dispensers according to the invention tool are shown.
Fig. 2: showing mixing chamber according to the present invention, and core is located at three different positions.
Fig. 3: showing selectable mixing chamber according to the present invention, and core is located at three different positions.
Fig. 4: the temperature in 298 ° of K, CO are shown2The saturated concentration dependent on pressure in water and ethyl alcohol (EtOH).
Fig. 5: show (a) mixing chamber according to the present invention the perspective sectional view and (b) to (d) is according to the present invention can
The mixing chamber of selection designs.
Fig. 6: the various embodiments for the translation mechanism along longitudinal axis translation core are shown.
Fig. 7: the embodiment party for controlling core position according to the composition for the concentrate being loaded in distribution utensil is shown
Case.
Detailed description of the invention
As shown in fig. 1, dispensers according to the invention tool uses as follows.Container (1) includes the fermentation drink based on malt
Expect (MBFB) concentrate, and is in fluid communication with mixing chamber (2).Carbonic acid diluent source (4) and identical mixing chamber are in fluid communication.
After mixing MBFB concentrate with soda, the MBFB so generated leaves from the outlet (2d) of mixing chamber, by dividing
Piping (5) is assigned in vessel (10), and vessel (10) can be glass or jar.Particularly, main points of the invention are related to using
In the mixing chamber (2) of mixing MBFB concentrate and carbonic acid diluent.Mixing chamber is defined by wall, and by perpendicular in longitudinal axis X
Between plane M1 be divided into upper and lower part: mixing chamber further include:
(a) concentrate opening (1d) is located in top and is provided with for the fixed container for accommodating MBFB concentrate
Fixation device；
(b) diluent openings (4d) is located in top and is provided with the dilution for connecting with carbonic acid diluent source
Agent interconnecting piece,
(c) export (2d), be parallel to longitudinal axis X orient and be located at lower part in, for discharge include MBFB concentrate and
The MBFB of the mixture of carbonic acid diluent,
(d) core (2c), is defined by wicking surface and is mounted in room, so that wicking surface defines flowing together with the wall of room
Channel (2p), the flow channel have the width w measured perpendicular to wicking surface.
As shown in Figures 2 and 3, core is movably mounted in room, and core is translated along longitudinal axis X, to control
The width w of the part of flow channel processed.Fig. 2 and Fig. 3 show core different location and flowing when with different configuration it is logical
The width in road.Three different locations of the core relative to mid-plane M1: (a) middle position wim are shown in Fig. 2 and Fig. 3, (b)
Upper position wiu, and (c) lower position wid, wherein i=1 or 2, wherein i=1 indicates being located at top of flow channel
Part, and i=2 indicates the part of flow channel being located at lower part.As above for corresponding pressure defined in width
Pij is also shown in figure, wherein i=1 or 2, and j=m, u or d.
When the single container (1) comprising MBFB concentrate is shown in FIG. 1, more than one container can be used, each
Container includes the different component in conc forms.One container can also include several rooms, and each room includes corresponding concentration
Component.The present invention is not limited to the number of container and forms.MBFB concentrate is in liquid form (or paste), makes it possible to and is pressing
Mixing chamber is flowed into from container under power.MBFB concentrate may include solid particle, but they must suspend in liquid medium.
Container may include a certain amount of MBFB concentrate, and the MBFB concentrate of the amount is sufficient to the list being assigned in a glass
Sub-distribution operates (single-dose containers), or selectively, may include a certain amount of MBFB concentrate, and the MBFB of the amount is dense
Contracting object is sufficient to carry out repeated dispensing operation (=multi-dose container).The latter is packaged into per unit volume MBFB concentrate
Present aspect is more economical.
The MBFB concentrate accommodated in container (1) can be by a conventional manner (for example, for beer, by with ability
Any mode beer brewing known to domain) production fermented beverage, the fermented beverage that so produces is concentrated then to obtain.Concentration is logical
It crosses and on the one hand removes a part of water contained therein and on the other hand remove a part of ethyl alcohol contained therein and occur.It uses
Suitable film well known to those skilled in the art can remove a large amount of water by filtering, micro-filtration, ultrafiltration or nanofiltration from beverage
Both with ethyl alcohol.
Flowing into the MBFB concentrate in mixing chamber can be only by gravity drive, and is controlled by valve (not shown).
But this embodiment is not preferred, because it will force the flowing of carbonic acid diluent also by gravity drive, so as to logical
Pressure drop sharply is not generated to the level height of the diluent openings of mixing chamber.It is therefore preferable that with pump (not shown) or
By by means of gas-pressurized (preferably pressurization CO2) source the flowing of MBFB concentrate is driven to the internal pressurization of container.
Gas-pressurized can be stored in pressurized tank (pressure canister) (3), as shown in Fig. 1 (a).Gas can use pump
(3p) pressurization, as shown in Fig. 1 (b).Selectively, if it is obtainable, then gas-pressurized can be obtained from network.It is important
Be the volume ratio that can control the MBFB concentrate and carbonic acid diluent that are fed into mixing chamber.It for this reason, can be with
Valve (not shown) is provided to control the flow of MBFB concentrate and carbonic acid diluent.Selectively, the volume flow of such as positive displacement pump
Amount controller can be used to control the volume of the MBFB concentrate and carbonic acid diluent that are fed into mixing chamber.
Carbonic acid diluent is a kind of liquid diluent, it includes CO2Amount be higher than in room temperature and CO under atmospheric pressure2
Solubility in the liquid diluent.This means that carbonic acid diluent is in room temperature and under atmospheric pressure by CO2Bubble rises
Bubble.Liquid diluent is preferably water.However, it is possible to use other liquid diluents substitute water.Particularly, have in quite
The beer of property mouthfeel is used as carbonic acid diluent.The aqueous solution that seasoning can also be used, for example, by using fruit-like flavour, such as
Cherry, peach and similar fruit, to produce fruit beer (fruity beer).Water has the advantages that big, i.e. carbonic acid diluent source
(4) it can be present in all families, equipped with the tap at carbonating station (carbonation station).If made
With pressurization CO2Cylinder (3) come drive MBFB concentrate flow into mixing chamber in, then identical pressurization CO can be used2Cylinder come carbonate from
Water.If water quality is unsatisfactory, filter can be used to handle the water flowed out from tap.If being different from carbonic acid
The carbonic acid diluent of water is used, then it can be stored in vessel (not shown).
As in Fig. 4 it can be noted that CO2Solubility in water sharp increases (empty bent very much with increased pressure
Line), wherein having about 0.1mol.% (molar percentage) to 0.2mol.%CO in 2.5 Ba Chu2。CO2In straight alcohol (EtOH)
Solubility (=solid-line curve) with higher, wherein being about 1.6mol.% at 2.5 bars of uniform pressure.Appointing including ethyl alcohol
It includes CO between this two curves that aqueous diluent, which will generate,2Solubility.The curve of Fig. 4 is shown, in carbonic acid diluent
Any variation of pressure all may cause CO2Blistering or dissolution.This is especially true for water is as liquid diluent,
Because the linear dash line in Fig. 4 has very steep slope.This be for MBFB it is vital because different from soda water,
Foam is kept for a long time after its formation.
It is the committed step distributed in utensil that carbonic acid diluent and MBFB concentrate, which enter mixing chamber, because in mixing chamber
It is likely to occur very big pressure drop, causes even to be assigned to being prematurely formed for foam before vessel (10) in beverage.Mixing chamber
Design can be optimized for a type of MBFB, but distribution of the customer to the MBFB that can only distribute very limited number
Utensil is dissatisfied.Customer requirement selects MBFB's from being generated in new beverage or multi-product option of comforming in different concentrates
Freely.Every kind of MBFB concentrate and every kind of carbonic acid diluent will differently react when mixing in mixing chamber, and a kind of recipe
It will lead to be formed than desired more foams, and another recipe will generate insufficient formation of foam.
As shown in Figures 2 and 3, using the core (2c) in the moveable mixing chamber of longitudinal axis X, the width of flow channel (2d)
Degree w can change at the selected part of the flow channel.Width w is open and diluent openings (1d, 4d) from concentrate
Be not necessarily on to the entire flow channel of the outlet (2d) of mixing chamber it is constant and it is usual be never constant.Flow channel
Design must assure that the outlet and being introduced into for reaching distribution pipe (5) in working fluid desirably form foam vessel (10) it
Before, do not occur unexpected pressure drop in working fluid.This can be by being avoided any sharp ladder (sharp in the stream of channel
Step) Lai Shixian.Flow channel, which can be, to be locally tapered, it is preferred that at least 70% wicking surface is generally flat
Row is in the wall of room.It is also preferred that concentrate opening (1d) and diluent openings (4d) be located at mix locular wall at so that core along
The translation on longitudinal axis X towards top reduce flow channel at concentrate opening and the level height of both diluent openings
Partial width w.Embodiment illustrated illustrates the preferred embodiment in Fig. 2, Fig. 3, Fig. 5 and Fig. 6.Concentrate opening and
Both diluent openings are located at the identical wall of the upper surface towards wicking surface, wherein in addition to Fig. 5 (c) and Fig. 5 (d) it
Outside, the upper surface is generally plane and perpendicular to longitudinal axis X.Term " on " is defined relative to mid-plane M1, and mixed
The mode that the top of conjunction room is defined is identical.In the accompanying drawings, longitudinal axis X is vertical and term " on " corresponds to " on vertically
Side ", but since mixing chamber is pressurization, so longitudinal axis X does not force to be vertical.In this case, statement " top " refers to
Be mixing chamber include concentrate opening and diluent openings (1d, 4d) part, the part is in (virtual) mid-plane
" lower part " at the level height of M1 with the outlet (2d) for including mixing chamber separates.
It is also preferred that longitudinal axis X passes through the outlet (2d) of mixing chamber.Other than opening and outlet, the wall of mixing chamber is excellent
Selection of land defines the geometry around longitudinal axis X rotation.All sharp edges in mixing chamber be preferably rounding to flow
Reducing pressure drop when crossing such ridge, (attached drawing is schematical, and including many sharp edges, preferably avoids point in practice
Sharp edge).The lower surface (that is, part of the outlet (2d) towards mixing chamber of wicking surface) of core, which preferably has, to be tapered
Geometry.The geometry being tapered can be cone, the vertex of the outlet towards mixing chamber of cone and vertical
Axis X alignment, as shown in Figures 2 and 3.Selectively, the geometry being tapered may include pear shape, more complicated
Shape, the pear shape as shown in Fig. 5 (c), or by bending generator (curved as shown in Fig. 5 (b)
Generator) the rotary volume generated.Core even can have the spherical geometries as shown in Fig. 5 (d), or oval
Shape or analogous shape.
By locally changing the width w of flow channel (2p), it can control and formed by concentrate and carbonic acid diluent
The pressure of liquid mixture.This is for controlling CO2The amount of blistering is critically important, and importantly, for controlling CO2Start
Bubble and the position for forming foam are critically important.As shown in Figures 2 and 3, the pressure Pij in liquid with flow channel width
Wij locally changes, wherein i=1 or 2, refers to two positions in flow channel, under 1 is located in top, and 2 are located at
It relative to mid-plane M1 is m=placed in the middle depending on core in portion, and wherein j=m, u or d, (b) upwards or (c) downwards.Fig. 2
(a) and Fig. 3 (a) is shown in which core in embodiment placed in the middle on mid-plane M1.This construction, which corresponds to, wherein flows road
The width w of diameter is the position for most uniformly (having minimum variation).The width w1m of flow channel is in top, neighbouring concentration
Object opening and diluent openings, and width w2m, in the lower part of flow channel, the pressure in working fluid is P1m and P2m.
In Fig. 2 (b) and Fig. 3 (b), core translates in upper direction along longitudinal axis X, this is compared with core placed in the middle on top
The width at place reduces, w1u<w1m, and the width at lower part correspondingly increases, w2u>w2m.Therefore, at top
Pressure is higher than the pressure of core placed in the middle, P1u > P1m.MBFB from distribution pipe (5) leave be assigned before, pressure P2u reduce, and
And some CO are formed in mixing chamber2Bubble is possible.
In Fig. 2 (c) and Fig. 3 (c), core is translated up along longitudinal axis X in lower part side, this increases compared with core placed in the middle
Width, w1d>w1m, but the width at lower part reduces, w2d<w2m.It therefore follows that pressure P1d and P2d is entirely being mixed
Remained in the flow channel of room it is high, and only when MBFB reach distribution pipe (5) and it is assigned when, pressure just declines.
As described above, the width w of flow channel can be changed by translating core along the longitudinal axis.In general, flow channel
Width can change between 0.1mm≤w≤10mm, preferably change between 0.5mm≤w≤5mm, more preferably 1mm
≤ w≤3mm variation.In some cases, core can seal concentrate opening and diluent openings, or selectively sealing mixing
The width w of the outlet of room can locally reach 0mm (that is, wall of wicking surface contact mixing chamber).
With the translation of core, the foam for the MBFB being assigned or the level of foaming can control.The level of the foam
Of course depend upon the taste of user.Its parameter for also relying on the control beyond user and appliance manufactures.Particularly, especially
It depends on:
The pressure of MBFB concentrate and carbonic acid diluent when they are flowed into mixing chamber,
CO in carbonic acid diluent2Concentration,
CO in MBFB concentrate2Concentration is (if condensate container CO2It pressurizes, then some CO2It will be dissolved
In MBFB concentrate),
Liquid diluent with such as following property: the CO of the liquid diluent2Saturated concentration and the CO2It is full
With the pressure dependency of concentration；
The composition of MBFB concentrate,
Temperature in mixing chamber.
Each new MBFB composition is characterized by one group of foregoing parameter values of their own.All these values can be
Variation in a certain range, at least insofar, the range are too wide and too complicated without allowing according to desired foaming water
Flat automatic pressure regulation.It therefore follows that having the distribution utensil for the mixing chamber width being sized may only satisfactorily divide
MBFB with the limited option with suitable foam level.By the core that it is moved, the present invention allows to adjust distributor
The property of tool allows to limit optimal allocation condition, this allows to distribute a variety of of the foam formation with required level
MBFB.The MBFB composition new for every kind, it must be determined that the optimum position of core, to distribute the foam-like with desired amount
The MBFB of object.After the optimum position of core has been found, as long as distribute identical MBFB composition (as long as and
Temperature, CO in carbonic acid diluent and MBFB concentrate2Concentration and pressure do not change), core is just fixed and does not need
It moves again.When needing new MBFB composition, it is necessary to determine best core position again, as explained below.It can establish
Database, the database provide the best core position range for the MBFB composition option for being suitable for establishing in advance.
Core can be translated by any of mode along longitudinal axis X.For example, core can couple as shown in Fig. 6 (a)
To the guide rail for being provided with rack gear.Pinion gear (2t) can be connected to track, and can drive with hand or with motor.It may be selected
Embodiment in, as shown in Fig. 6 (b), can manually translate core with control stick.It is preferably implemented shown in Fig. 6 (c)
In scheme, linear motor can be used, coil (2m) is wound around mixing chamber, and core includes magnet.Aforementioned translation
Mechanism is only used as illustrative example to quote, and can be alternatively using other mechanisms for translating core.
In selectable embodiment, the position of core can be controlled by the container (1) of receiving concentrate.Because from basis
Distribution utensil of the invention leaves the composition that the foam levels formed when distribution MBFB are strongly depend on concentrate, so core is pre-
If position can be associated with the composition of given concentrate.In order to implement the embodiment, every other allocation of parameters is certain
It must be according to preset condition, including at carbonic acid diluent, carbonic acid diluent source and the pressure in condensate container etc..For example,
As shown in Figure 7, coupling arrangement (72), the connection has can be set in the part for being directly facing concentrate opening (1d) of wicking surface
Device (72) is suitable for being reversibly coupled to be mounted on the complementary connecting device (71) on condensate container (1).Complementation connection dress
The opening from condensate container is set to extend away from given distance LA, LB of the opening.Distance LA, LB is preparatory in the factory
Determining, type A, B dependent on the concentrate accommodated in condensate container.When condensate container (1) is fixed to distribution
When the fixation device and complementary connecting device of utensil are reversibly coupled to core coupling arrangement, distance LA, LB define core along
The position of longitudinal axis X.
Complementary connecting device may be mounted at one end of the bar (stem) with predetermined length LA, LB.Bar is not
It needs to be rigid, this depends on the type of used (complementation) coupling arrangement (71,72).For example, core and complementary connection dress
Setting (71,72) can be magnet.In this case, bar can be flexible, and can be replaced with rope.Core and complementary connection
Connection device (71,72) can be external screw thread/internal screw thread screw, can consolidate between condensate container and mixing chamber
Determine device combination, which also includes similar screw thread.By via the band spiral shell that condensate container is screwed in distribution utensil
The condensate container is fixed on the fixation device of line, it is fixed device (72) that complementary fixture (71) will simultaneously engage with core.When
Also can be there is a situation where same when unscrewing empty container, which will be such that complementary connecting device and core coupling arrangement is detached from simultaneously.
Fig. 7 illustrates two condensate containers for accommodating concentrate A and concentrate B.Distance LB ratio for concentrate B is used
In the distance LA long of concentrate A.Therefore, when the container of concentrate B is fixed to the fixation device of distribution utensil and alternatively
It is compared when the container of concentrate A is installed, core is further pushed to the lower part of mixing chamber, wherein distance LA < LB.Therefore, when dense
Contracting object B compared with when alternatively using concentrate A, generates higher back pressure when the mixing of carbonic acid diluent in mixing chamber, and
And CO2It keeps dissolving the section that lasts much longer in the mixture.
As schematically shown in Fig. 5 (a), structural elements (2s) has been can be set in wicking surface, such as in continuously or not
Continuous groove or the protruding portion or recess of ridged formula, the shape in point, pod-like object (beans), baffle (baffles)
Discrete protruding portion or recess, the protruding portion with the convex or recessed geometry towards mixing chamber top and similar
Structural elements.The structured surface of core can help direct fluids to flow with desired mode, and enhance carbonic acid diluent
With the mixing of MBFB concentrate.When designing such structured surface, it is necessary to not damage the clear of mixing chamber after careful use
It is clean.May alternatively or additionally, the wall of mixing chamber can be structured (not shown) as described in above for core.
Mixing chamber must be cleaned periodically.This can be by the way that after the batch operation of given number, the flushing with such as water be molten
Liquid (may have detergent) rinses it to complete.It, can be in no CO if liquid diluent is water2In the case where lead to
It crosses diluent openings (4d) to be injected, with cleaning down mixing chamber.Selectively, additional flushing opening (6) can be set
In mixing chamber, and it is connected to flushing liquid source.Detergent can be used dedicated for rinsing in flushing opening.It rinses
Being open (6) can be at the wall towards core of mixing chamber, or as shown in Fig. 5 (b), can be located at the wall of mixing chamber
Place forms tubular fluid connection without being directly facing core between fixed device and core.This embodiment is interesting, because
Tubular fluid interconnecting piece as rinse solution.Valve ensures that MBFB concentrate does not pass through flushing opening outflow.Such as institute in Fig. 5 (c)
Show, diluent openings can also be located in the wall of such tubular fluid interconnecting piece.
The present invention relates to distribution utensils itself.Certainly, further relate to distribution utensil below: the distribution utensil, which has, to be fixed
To fixed device, receiving MBFB concentrate container, and it is connected to the carbonic acid diluent source of diluent interconnecting piece, preferably
Carbonated water.It so loads and the distribution utensil of the invention of connection is operable and can be used to distribute with best bubble
The MBFB of the amount of foam shape object.If distributing utensil includes electric drive function, it is necessarily connected to power supply certainly.For example, distribution
Utensil may include for cooling down the cooling unit of carbonic acid diluent, electrodynamic pump, flow controller, valve etc..
The invention further relates to for controlling the foam formed during the distribution of the fermented beverage (MBFB) based on malt
The method of amount, the described method comprises the following steps:
(a) distribution utensil as discussed above is provided, the distribution utensil is with fixed to fixed device, receiving MBFB is dense
The container of contracting object, and it is connected to the carbonic acid diluent source of diluent interconnecting piece；
(b) core is set as the initial position relative to mid-plane M1,
(c) with predetermined volume ratio by MBFB concentrate and carbonic acid diluent injection mixing chamber, and by small size as
This MBFB formed leaves from outlet to be assigned in container (10)；
(d) level of the foam formed in accommodating MBFB in a reservoir is assessed,
If (e) level of foam is not corresponding with desired level, X translates core in a longitudinal direction, and
(f) level of step (a) to step (d), until reaching desired foam is repeated.
These operations seem pretty troublesome, but they carry out quickly, and are easily found and provide desired foam
The optimum position of the core of shape object level, and the very limited waste with beverage.After finding the correct position of core, as long as
Using identical component and distributive condition, can be maintained at the position.
Claims (12)
1. a kind of distribution utensil, for by fermented beverage (MBFB) concentrate based on malt is mixed with carbonic acid diluent come
Preparation and distribution MBFB, the distribution utensil include the mixing chamber for mixing the MBFB concentrate and the carbonic acid diluent
(2), the mixing chamber is defined by wall and is divided into upper and lower part, the mixing chamber by the mid-plane M1 perpendicular to longitudinal axis X
Include:
(a) concentrate opening (1d), the concentrate opening (1d) is located in the top and is provided with to be accommodated for fixed
The fixation device of the container of MBFB concentrate；
(b) diluent openings (4d), the diluent openings (4d) are located in the top and are provided with and carbonic acid diluent
The diluent interconnecting piece of source connection,
(c) (2d) is exported, the outlet (2d) is parallel to the longitudinal axis X and orients and be located in the lower part, for discharging packet
The MBFB of the mixture of MBFB concentrate and carbonic acid diluent is included,
(d) core (2c), the core (2c) are defined by wicking surface and are installed in the chamber, so that the wicking surface and the room
The wall define together flow channel (2p), the flow channel (2p) has the width w that measures perpendicular to the wicking surface,
It is characterized in that, the core is movably mounted in the room, the core is translated along the longitudinal axis X,
So as to control the flow channel part width w.
2. distribution utensil according to claim 1 further includes the flue that may be connected to the source of gas-pressurized, the gas
Pipe is arranged so that the outlet and the inside of the container for the receiving MBFB concentrate for being fixed to the fixed device of the flue
It constitutes and is in fluid communication.
3. distribution utensil according to claim 1 or 2, wherein the core can be one of in the following manner along described vertical
Axis translation:
Manually or by motor driving rack-and-pinion,
Control stick；Or
Linear motor.
4. the distribution utensil according to any one of preceding claims 1 to 3, wherein the geometry of the core make it is described
At least the 70% of wicking surface is substantially parallel to the wall of the room.
5. distribution utensil according to claim 4, wherein the core subtracts along the translation on the longitudinal axis X towards the top
The width w of part of the small flow channel at the level height of both concentrate opening and diluent openings.
6. the distribution utensil according to any one of preceding claims 1 to 5, wherein the width w of the flow channel can
By translate the core between 0.1mm≤w≤10mm, preferably between 0.5mm≤w≤5mm, more preferably 1mm≤w≤
Change between 3mm.
7. the distribution utensil according to any one of preceding claims 1 to 6, wherein concentrate opening and the dilution
Both agent openings are both provided with volumetric flow controller.
8. the distribution utensil according to any one of preceding claims 1 to 7, wherein the wicking surface and/or the mixing
The wall of room is configured to protruding portion and/or recess (2s).
9. the distribution utensil according to any one of preceding claims 1 to 8, wherein the container for accommodating MBFB concentrate is consolidated
Surely the fixed device is arrived, and the source of the carbonic acid diluent of preferably carbonated water is connected to the diluent interconnecting piece.
10. according to distribution utensil described in claim 2 and 9, wherein the source of the preferably gas-pressurized of CO2 be connected to it is described
Flue.
11. the distribution utensil according to any one of preceding claims 1 to 10, wherein the wicking surface is directly facing institute
The part for stating concentrate opening is provided with core coupling arrangement (72), and the core coupling arrangement (72) is suitable for being reversibly coupled to mutually
It mends coupling arrangement (71), the complementary connecting device (71) is mounted on condensate container (1) and from the condensate container
Opening extend predetermined distance, when the condensate container is fixed to the fixed device and when it is described mutually
It is described predetermined when benefit coupling arrangement is reversibly coupled to the core coupling arrangement at the part of the wicking surface
Distance defines the core along the position of the longitudinal axis X.
12. a kind of method for controlling the amount of the foam formed during the distribution of the fermented beverage (MBFB) based on malt,
It the described method comprises the following steps:
(a) the distribution utensil according to claim 9 or 11 is provided；
(b) core is set as the initial position relative to the mid-plane M1,
(c) MBFB concentrate and carbonic acid diluent are injected in the mixing chamber with predetermined volume ratio；And by what is be thusly-formed
MBFB is assigned in container from the outlet；
(d) level of the foam formed in accommodating the MBFB in the above-described container is assessed,
If (e) level of the foam is not corresponding with desired level, X translates the core in a longitudinal direction, and
(f) level of step (a) to step (d), until reaching desired foam is repeated.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP16196358.2 | 2016-10-28 | ||
| EP16196358.2A EP3315458A1 (en) | 2016-10-28 | 2016-10-28 | Dispensing appliance for the control of froth formation during dispensing of a malt based fermented beverage (mbfb) produced in situ by mixing an mbfb concentrate with a carbonated diluent |
| PCT/EP2017/077423 WO2018078007A1 (en) | 2016-10-28 | 2017-10-26 | Dispensing appliance for the control of froth formation during dispensing of a malt based fermented beverage (mfbf) produced in situ by mixing an mbfb concentrate with a cabonated diluent |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110121479A true CN110121479A (en) | 2019-08-13 |
Family
ID=57211386
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201780080744.0A Pending CN110121479A (en) | 2016-10-28 | 2017-10-26 | For controlling the distribution utensil of the formation of foam during the distribution by fermented beverage (MFBF) concentrate of the mixing based on malt and the MBFB of carbonic acid diluent produced in situ |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US20190241420A1 (en) |
| EP (2) | EP3315458A1 (en) |
| JP (1) | JP2019532881A (en) |
| KR (1) | KR20190084064A (en) |
| CN (1) | CN110121479A (en) |
| AR (1) | AR109878A1 (en) |
| AU (1) | AU2017350303A1 (en) |
| BE (1) | BE1025836B1 (en) |
| BR (1) | BR112019008586A2 (en) |
| CA (1) | CA3041943A1 (en) |
| MX (1) | MX2019004700A (en) |
| RU (1) | RU2745422C2 (en) |
| WO (1) | WO2018078007A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115461138A (en) * | 2020-03-27 | 2022-12-09 | 高仪股份公司 | Dispensing cartridge |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11751585B1 (en) | 2022-05-13 | 2023-09-12 | Sharkninja Operating Llc | Flavored beverage carbonation system |
| US11745996B1 (en) | 2022-11-17 | 2023-09-05 | Sharkninja Operating Llc | Ingredient containers for use with beverage dispensers |
| US11634314B1 (en) | 2022-11-17 | 2023-04-25 | Sharkninja Operating Llc | Dosing accuracy |
| US11738988B1 (en) | 2022-11-17 | 2023-08-29 | Sharkninja Operating Llc | Ingredient container valve control |
| US11871867B1 (en) | 2023-03-22 | 2024-01-16 | Sharkninja Operating Llc | Additive container with bottom cover |
| US11925287B1 (en) | 2023-03-22 | 2024-03-12 | Sharkninja Operating Llc | Additive container with inlet tube |
| US11931704B1 (en) | 2023-06-16 | 2024-03-19 | Sharkninja Operating Llc | Carbonation chamber |
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-
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- 2017-10-25 AR ARP170102960A patent/AR109878A1/en active IP Right Grant
- 2017-10-26 MX MX2019004700A patent/MX2019004700A/en unknown
- 2017-10-26 BR BR112019008586A patent/BR112019008586A2/en not_active Application Discontinuation
- 2017-10-26 KR KR1020197015163A patent/KR20190084064A/en not_active Application Discontinuation
- 2017-10-26 AU AU2017350303A patent/AU2017350303A1/en not_active Abandoned
- 2017-10-26 US US16/345,667 patent/US20190241420A1/en not_active Abandoned
- 2017-10-26 JP JP2019522529A patent/JP2019532881A/en active Pending
- 2017-10-26 RU RU2019113048A patent/RU2745422C2/en active
- 2017-10-26 WO PCT/EP2017/077423 patent/WO2018078007A1/en unknown
- 2017-10-26 CN CN201780080744.0A patent/CN110121479A/en active Pending
- 2017-10-26 EP EP17797100.9A patent/EP3532427A1/en not_active Withdrawn
- 2017-10-26 BE BE20175767A patent/BE1025836B1/en not_active IP Right Cessation
- 2017-10-26 CA CA3041943A patent/CA3041943A1/en not_active Abandoned
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| US2558700A (en) * | 1946-10-30 | 1951-06-26 | Marion L J Lambert | Carbonated beverage dispensing valve |
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Also Published As
| Publication number | Publication date |
|---|---|
| EP3532427A1 (en) | 2019-09-04 |
| EP3315458A1 (en) | 2018-05-02 |
| KR20190084064A (en) | 2019-07-15 |
| MX2019004700A (en) | 2019-09-18 |
| RU2019113048A3 (en) | 2021-01-22 |
| BE1025836A1 (en) | 2019-07-19 |
| RU2019113048A (en) | 2020-11-30 |
| BE1025836B1 (en) | 2019-09-19 |
| WO2018078007A1 (en) | 2018-05-03 |
| US20190241420A1 (en) | 2019-08-08 |
| RU2745422C2 (en) | 2021-03-25 |
| AR109878A1 (en) | 2019-01-30 |
| CA3041943A1 (en) | 2018-05-03 |
| JP2019532881A (en) | 2019-11-14 |
| BR112019008586A2 (en) | 2019-07-09 |
| AU2017350303A1 (en) | 2019-05-23 |
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Application publication date: 20190813 |